New eco-friendly proposal for the crystallization of beet raw juice

In the past years we evaluated different strategies with the aim of eliminating completely from the beet sugar factory, the traditional calco-carbonic purification process taking into account the well-known problems related to the utilization of lime and the production of carbonation sludge.To complete the picture of the possible solutions to be adopted for the elimination of the traditional purification process, we tested and evaluated in laboratory and in pilot plants a new eco-friendly proposal.The results obtained, as well as the proposed flow-sheet and some economic evaluations, are presented and discussed.     

管式电除尘器“伞形罩”结构的应用

本文通过分析立式管式电除尘器结构及使用现状 ,总结其失效的主要原因在于阳极 (圆筒管 )的清灰不力。为解决清灰不力的问题 ,提出了“伞形罩”阳极结构 ,其具有的不积尘、自动排灰功能 ,经实践检验 ,效果显著     

Shellac-coated iron oxide nanoparticles for removal of cadmium(II) ions from aqueous solution

This study describes a new effective adsorbent for cadmium removal from aqueous solution synthesized by coating a shellac layer, a natural biodegradable and renewable resin with abundant hydroxyl and carboxylic groups, on the surface of iron oxide magnetic nanoparticles. Transmission Electron Microscopy (TEM) imaging showed shellac-coated magnetic nanoparticle (SCMN) adsorbents had a core-shell structure with a core of 20 nm and shell of 5 nm. Fourier Transform Infrared Spectroscopic analysis suggested the occurrence of reaction between carboxyl groups on the SCMN adsorbent surface and cadmium ions in aqueous solution. Kinetic data were well described by pseudo second-order model and adsorption isotherms were fitted with both Langmuir and Freundlich models with maximum adsorption capacity of 18.80 mg/g. SCMN adsorbents provided a favorable adsorption capacity under high salinity conditions, and cadmium could easily be desorbed using mild organic acid solutions at low concentration.     

实时合成水滑石分离模拟放射性核素锶的研究

采用实时合成水滑石的方法从高放废液中分离模拟放射性核素锶,通过单因素实验并借助XRD分析确定了最佳分离实验条件,同时,运用FTIR、SEM等技术手段对合成的含锶水滑石的结构、形貌进行了分析.结果表明,当Sr2+初始浓度为70mg.L-1、pH值为10.5、n(Mg+Sr)/n(Al)为3时,锶的去除率最高可达95%以上;XRD和SEM分析结果表明,锶嵌入了水滑石的晶格中,合成的含锶水滑石形貌为层状六边形;含锶水滑石煅烧产物主要为尖晶石,且煅烧产物中未见氧化锶,表明嵌入到水滑石晶格中的锶在煅烧后存在于尖晶石的晶体结构中.     

混合气体直接吸附分离回收过程研究

以精密陶瓷制造过程中排放的甲苯和异丙醇混合气体为目标气体,采用4段活性炭吸附柱串联吸附实验方式研究了混合组分气体直接吸附分离回收的可行性.结果表明,异丙醇和甲苯这2种物性具有一定差异的物质在吸附床的长度方向存在明显的分层吸附现象.在表观气速0.42 m·s-1、异丙醇与甲苯入口浓度分别为477 mg·m-3和746 mg·m-3、吸附柱总长为26cm条件下,通气吸附798 min时,0～10 cm长度段炭层吸附甲苯量为184.5 mg·g-1,吸附异丙醇量为0 mg·g-1,而21～26 cm长度段炭层吸附甲苯量为0.92 mg·g-1,吸附异丙醇量为91.2 mg·g-1,通过分段再生回收分别得到了纯度99%以上的甲苯和异丙醇回收液.弱吸附质异丙醇在吸附过程中存在气相浓度增浓现象,该现象导致实验条件下部分活性炭层区域对异丙醇的吸附量提高了27%以上.通过多段串联吸附、分段再生回收的方式可以实现混合气体的直接吸附分离回收.     

印染废水RO浓水水质分析

以江苏某印染废水处理厂反渗透（RO）浓水为研究对象,采用多种分析手段分析了RO浓水的水质特征.首先采用IC和ICP-MS对水中的无机离子进行了定性和定量分析,采用GC-MS对废水中的半挥发性有机物进行定性和定量分析.结果表明,RO浓水中无机离子以Na⁺、Cl^-和SO₄^2-为主,半挥发性有机物邻苯二甲酸二（2-乙基己）酯（DEHP）为主要成分,其浓度为1.452mg/L.为分析RO浓水中的溶解性有机物（DOM）特征,进一步采用超滤膜分子量分级法和树脂亲疏水分离技术对废水中的DOM进行分离解析,分析了不同组分的溶解性有机碳（DOC）、UV₂₅₄、SUVA含量和分布情况,应用三维荧光光谱对各组分物质进行了定性分析.超滤分级表明,RO浓水中相对分子量<1k的有机物占56.98%,相对分子质量5~10k有机物仅占2.19%,但其芳香化程度较高.树脂分离结果表明,RO浓水中亲水性物质（HPI^*）、疏水性物质（HPO^*）和过渡性物质（TPI^*）的DOC含量差异不大,其中HPO^*的芳香构造化程度最高,含有较多的色氨酸类芳香族蛋白质,而HPI^*中含有较多的溶解性微生物代谢产物类物质.     

电解浮选用于活性污泥固液分离的研究

在装有Ti/RuO₂-IrO₂-TiO₂阳极、Ti阴极的电解浮选槽中进行了活性污泥固液分离的研究.考察了影响电解浮选性能的操作参数,这些参数包括水力停留时间、电流密度、进水SS浓度和进水pH值.研究表明,电解浮选是高效的固液分离单元,水力停留时间和电流密度是主要的影响因素.SS的去除率随着水力停留时间和电流密度的增加而增大;污泥负荷增加,SS的去除率下降;pH值影响电解产生微气泡的尺寸和污泥性质,但对SS的去除影响不大,实际应用中可以不调节pH值.进水SS约1 000mg/L时,当水力停留时间为20min,接触室电流密度为5 mA/cm²,分离区电流密度为2.5 mA/cm²,SS的去除率可达97%以上,此时的能耗为0.4～0.5(kW.h)/m³废水.电解浮选产生的浮渣含水率为95.9%,低于溶气气浮和二沉池的污泥含水率,对污泥减量化及其最终处置有较大的意义.     

膜吸收器吸收CO2的影响因素研究

采用聚丙烯中空纤维膜吸收器,用水、NaOH和K2CO3 水溶液作为吸收剂进行高浓度CO2 吸收试验,考察了气体流率、吸收剂流率、质量分数以及流动方式对吸收率、传质系数和传质速率的影响.结果表明,随着气体流率增大,CO2的吸收率递减,总传质系数和总传质速率增加.在一定的气体流率下,吸收液流率增大,CO2的吸收率、总传质系数和总传质速率增大;吸收液浓度提高,吸收率增大,总传质系数和总传质速率提高.在气体流率较低时,质量分数为5%和8%的NaOH水溶液为吸收剂时的吸收率、总传质系数和总传质速率比较接近.随着气体流率增大,NaOH质量分数为8%时的吸收率、总传质系数和总传质速率增加的值大大超过NaOH质量分数为5%时增加的值.以水为吸收剂时,气体与吸收剂的流动方式为逆流时的吸收率、总传质系数和总传质速率高于并流时的值.     

Influence of super-absorbent polymer on the growth rate of gas hydrate

The growth rate of hydrate and morphology of methane hydrate formation were studied in a visual pressure cell at 5.5 MPa. The gas hydrate formation was carried out (coal mine methane (CMM) + tetrahydrofuran (THF) + sodium dodecyl sulphate (SDS) + H₂O) with and without SAP. Experimental data on the hydrate growth rate and induction time were obtained for three different CMM samples. The influence of SAP on hydrate growth rate was determined. Results showed that after the addition of SAP, with the methane concentration increased in CMM, the induction time was reduced by 9 min, 10 min and 3 min, and the growth rate was shortened by 0.56 × 10⁻⁶/m³ min⁻¹, 0.53 × 10⁻⁶/m³ min⁻¹ and 1.42 × 10⁻⁶/m³ min⁻¹, respectively. This study could be useful for the recovery of methane from CMM by forming hydrate in the chemical and mining industry.